Process for the production of zeolitic alkali metal aluminosilicates
AssigneesHenkel Kommanditgesellschaft auf Aktien, Deutsche Gold- und Silber-Scheideanstalt vormals Roessler
InventorsPeter Christophliemk, Wolfgang Friedemann, Ernst Vaeth, Karl-Heinz Worms
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Abstract
A process for the production of zeolitic alkali metal aluminosilicates by the reaction of aqueous alkali metal silicate solutions with an aqueous alkali metal aluminate solution containing sulfate anions at temperatures of 0.degree. C to 110.degree. C under a shearing type of agitation and conversion of the amorphous precipitate to crystalline forms by maintaining an aqueous suspension of the amorphous form at temperatures of 40.degree. C or over for a time sufficient to effect crystallization, whereby formation of substantial amounts of inactive nosean are avoided.
Claims8
A process for the production of zeolitic alkali metal aluminosilicates from alkali metal aluminate solutions containing alkali metal sulfate impurities consisting essentially of the steps of
- a. mixing an aqueous alkali metal silicate solution with an aqueous alkali metal aluminate solution
- 1. containing an alkali metal sulfate having a molar ratio of Al.sub.2 O.sub.3 to sulfate of 1:0.35 to 1.25 under agitation at a precipitation temperature of from 0.degree. C to 110.degree. C,
- 2. in such amounts that the resulting mixture has a molar ratio of alkali oxide :
- Al.sub.2 O.sub.3 :
- SiO.sub.2 of 1.5 to 6.0:1.0:1 to 5.0, wherein
- 3. the alkali metal oxide is present in a stoichiometric excess with respect to SiO.sub.2,
- 4. the excess of alkali metal oxide over unity as well as the alkali metal oxide concentration is decreased when the sulfate content is increased, and
- 5. the alkali metal oxide :
- Al.sub.2 O.sub.3 :
- SiO.sub.2 solids content of the resultant aqueous mixture is maintained between 10% to 40% by weight,
- b. subjecting the aqueous precipitate to a homogenization by application of shearing forces,
- c. converting the amorphous homogenized slurry to a crystalline state by maintaining the slurry at a crystallization temperature of between about 40.degree. C and 120.degree. C,
- d. determining the calcium binding power of the crystalline aluminosilicate formed, and
- e. (6) discontinuing the conversion step (c) by cooling and separating the crystalline aluminosilicate when substantially the optimum calcium binding power is attained.
Dependencies are inferred from the claim text.